Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
  • B22F9/00—Making metallic powder or suspensions thereof
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
  • H01G4/00—Fixed capacitors; Processes of their manufacture
  • H01G4/002—Details
  • H01G4/005—Electrodes
  • H01G4/008—Selection of materials
  • H01G4/0085—Fried electrodes
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
  • B22F1/00—Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
  • B22F1/00—Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
  • B22F1/10—Metallic powder containing lubricating or binding agents; Metallic powder containing organic material
  • B22F1/107—Metallic powder containing lubricating or binding agents; Metallic powder containing organic material containing organic material comprising solvents, e.g. for slip casting
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
  • B22F1/00—Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
  • B22F1/16—Metallic particles coated with a non-metal
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
  • H01B1/00—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors
  • H01B1/20—Conductive material dispersed in non-conductive organic material
  • H01B1/22—Conductive material dispersed in non-conductive organic material the conductive material comprising metals or alloys
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
  • H01G4/00—Fixed capacitors; Processes of their manufacture
  • H01G4/30—Stacked capacitors
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
  • B22F2998/00—Supplementary information concerning processes or compositions relating to powder metallurgy
  • B22F2998/10—Processes characterised by the sequence of their steps
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
  • Y10T428/00—Stock material or miscellaneous articles
  • Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
  • Y10T428/2982—Particulate matter [e.g., sphere, flake, etc.]
  • Y10T428/2991—Coated

Definitions

• the present invention relates to a nickel powder, in particular suitable for forming electrodes in multilayer ceramic electronic components, such as multilayer capacitors, multilayer inductors, and multilayer actuators, to a conductive paste comprising the nickel powder, and a multilayer ceramic electronic component using same.
• a multilayer ceramic electronic component (also referred to hereinbelow as “multilayer electronic component”) is usually manufactured in the manner as follows.
• a ceramic starting material powder such as dielectric, magnetic, or piezoelectric powder is dispersed in a resin binder and molded into sheets to obtain ceramic green sheets (referred to hereinbelow as “ceramic sheets”).
• a conductive paste for an internal electrode that is prepared by dispersing an inorganic powder comprising an electrically conductive powder as the main component and optionally a ceramic powder or the like in a vehicle comprising a resin binder and a solvent is printed according to a predetermined pattern on the ceramic sheet and dried to remove the solvent and form a dry film of the inner electrode.
• a plurality of ceramic sheets each having the dry film for the inner electrode that were thus obtained are laminated and pressurized to obtain a non-fired laminate in which the ceramic sheets and paste layers of inner electrodes are alternately laminated.
• the laminate is cut to a predetermined shape, then subjected to a binder removal process in which the binder is burned and dissipated, and fired at a high temperature whereby sintering of the ceramic layers and formation of the inner electrode layers are conducted simultaneously and a ceramic body is obtained.
• Terminal electrodes are then fused to both end surfaces of the body and a multilayer electronic component is obtained. The terminal electrodes and the unfired multilayer body are sometimes co-fired.
• powders of base metals such as nickel and copper are mainly used instead of powders of noble metals such as palladium and silver as electrically conductive powders of conductive pastes for inner electrodes. Accordingly, firing of the laminate is usually carried out in a nonoxidizing atmosphere with an extremely low partial pressure of oxygen in order to prevent the oxidation of the base metal during firing.
• Patent Document 1 discloses a nickel powder having a mean particle size of 0.1 to 0.8 ⁇ m and an oxygen content of 0.5 to 5.0 wt.% and subjected to surface oxidation.
• Patent Document 2 discloses a nickel powder having an oxide surface thereon with a certain thickness and this document states that using such a surface-oxidized nickel powder raises the starting temperature of sintering shrinkage, and prevents delamination and cracking as well as the increase in resistance caused by over-sintering.
• the study conducted by the inventors demonstrated that although an oxidized layer formed on the nickel powder surface, such as described in Patent Documents 1 and 2, is effective in preventing structure defects and increase in the resistance value, the effect thereof is sometimes insufficient.
• a nickel powder which inherently has high catalytic activity, acts as a catalyst for decomposition of the resin binder and tends to accelerate the decomposition process.
• the mean particle size of the nickel powder is on the order of a submicron level, in particular, becomes 0.5 ⁇ m or less, the activity of the nickel powder itself further increases and part of the resin sometime explosively decomposes at a temperature lower than the usual resin decomposition temperature even when using the nickel powder subjected to surface oxidation by the method described in Patent Documents 1 and 2.
• Patent Document 1 Japanese Patent Publication No. 10-106351 A .
• Patent Document 2 Japanese Patent Publication No. 2000-45001 A .
• An object of the present invention is to resolve the above-described problems and to provide a nickel powder that has low activity despite an extremely small size and makes it possible to reduce the amount of residual carbon after the binder removal process when being used for forming an inner electrode, whereby the film thickness of the electrode can be reduced without causing the degradation of strength or electric characteristics of electronic components or the generation of structural defects.
• Yet another object is to provide a conductive paste containing the nickel powder and further to obtain a multilayer ceramic electronic component having high reliability and excellent electric characteristics by using the paste.
• the present invention has the following features.
• the amount of residual carbon after the binder removal process can be greatly reduced and degradation of properties or occurrence of cracks can be prevented even with an extremely fine powder with a mean particle size of 0.05 to 1.0 ⁇ m, in particular with a mean particle size of 0.5 ⁇ m or less.
• the decrease in the amount of residual carbon is apparently due to the decrease in catalytic activity of nickel and inhibited decomposition of resin at a low temperature that result from improved continuity and stability of the oxidized surface layer of the nickel powder.
• a multilayer ceramic electronic component with excellent continuity of electrode film, no structural defects, and excellent electric properties and strength can be obtained. Furthermore, a highly reliable multilayer ceramic electronic component can be obtained even in the case of highly multilayer articles with thin ceramic layers and thin inner electrode layers.
• the nickel powder in accordance with the present invention additionally contains a specific amount of sulfur, the activity of nickel can be further decreased, and because practically no sulfur component remains after firing, an excellent property improvement effect is demonstrated.
• the occurrence of undesirable decomposition of resin at a low temperature can be further prevented and the degradation of properties and occurrence of cracking can be prevented.
• a multilayer ceramic electronic component in which inner electrodes are formed by using the conductive paste is free of structural defects and has excellent electric properties and high reliability.
• a thin oxidized layer of nickel is formed on the surface, and the total amount of oxygen contained in the powder has to be 0.3 to 3.0 wt.%, in a proportion to the nickel powder. If the amount of oxygen is less than 0.3 wt.%, the thickness of the oxidized layer decreases and the surface cannot be uniformly coated. As a result the effect of decreasing the activity of nickel is reduced. Furthermore, if the amount of oxygen exceeds 3.0 wt.%, generation of gas and volume changes caused by the reduction of nickel oxide during firing in a reducing atmosphere increase and a dense electrode film cannot be obtained. At the same time, cracking and delamination of the multilayer electronic component are induced.
• the amount of oxygen in nickel powder is represented by ignition weight loss by heating in a reducing atmosphere (referred to hereinbelow simply as "ignition loss") which is measured as a weight variation percentage when the powder is heated from room temperature to 900°C in a reducing atmosphere composed of N 2 atmosphere containing 4% H 2 .
• the ignition loss measured by this method essentially includes all the components that are contained in the nickel powder and volatilized by heating, but because the content of volatile components other than oxygen, such as carbon, and sulfur, in the nickel powder in accordance with the present invention is extremely small by comparison with that of the amount of oxygen, the amount of oxygen in the nickel powder can be approximately represented by the ignition loss.
• the mean particle size of the nickel powder is less than 0.05 ⁇ m, the activity becomes too high and decomposition of resin at a low temperature or sintering of the nickel powder at a low temperature cannot be inhibited. Furthermore, when a conductive paste is manufactured, a large amount of organic components such as solvent and dispersant is necessary to disperse the nickel powder in the paste and obtain the adequate viscosity characteristic. As a result, a dense electrode dry film is difficult to obtain. Furthermore, in order to decrease the thickness of the inner electrode to meet the requirement relating to the miniaturization and increase in the number of laminated layers in multilayer electronic components, the mean particle size of nickel powder has to be 1.0 ⁇ m or less.
• the mean particle size of the powder represents a particle size calculated from a specific surface area measured by a BET method.
• the present invention is characterized in that the content of carbon in such nickel powder having an oxidized surface layer is controlled to an extremely low level.
• Japanese Patent Publication No. 2001-284161A discloses that if carbon is contained at 0.02 to 15 wt.% in a fine nickel powder with a mean particle size of 1.0 ⁇ m or less, the discontinuity and film thickness increase in the electrode are prevented and sintering is effectively delayed. However, when such a fine nickel powder was used in prior art, it was thought that the introduction of carbon into the nickel powder produced the effect of inhibiting the discontinuity and film thickness increase in the electrode.
• the apparent reason therefor is that a continuous and dense oxidized layer is maintained with good stability on the surface of nickel particles at least until the temperature at which the resin is decomposed at a low-temperature stage of the firing process is attained.
• the content of carbon be 80 ppm or less per specific surface area of 1 m 2 /g because an extremely good effect can be obtained. No restriction is placed on the lower limit of amount of carbon, and the lower is this amount, the better results are obtained.
• carbon is inherently contained as unavoidable impurity, it is technologically difficult to remove the carbon completely, and cost limitations are also applied.
• the amount of carbon be about 30 ppm to 80 ppm per specific surface area of 1 m 2 /g.
• the amount of carbon as referred to in accordance with the present invention is a sum total of all the carbon present inside the nickel powder and on the surface thereof and can be measured, for example, by a commercial carbon-sulfur analyzer.
• Carbon contained in the nickel powder includes carbon included as an unavoidable impurity from the nickel starting material and manufacturing process and also carbon that is introduced by an organic-system surface treatment conducted on the nickel powder.
• Such surface treatment is mainly conducted to increase dispersivity of the nickel powder in an organic vehicle when the nickel powder is used in a conductive paste. Practically in most of the treatment methods using an organic surface treatment agent that is effective in terms of increasing dispersivity, the treatment agent is strongly adhered to the nickel powder surface. Therefore, similarly to the carbon contained in the nickel powder, this agent adversely affects the oxidized surface layer.
• the specific surface area is a specific surface area measured by a BET method.
• the expression "100 ppm or less per specific surface area of 1 m 2 /g of the powder” means that if the specific surface area of the nickel powder is taken as a m 2 /g, then the carbon content is (a ⁇ 100) ppm or less based on the weight of the nickel powder, that is, 100 ⁇ 10 -6 g or less based on a surface area of 1 m 2 of the nickel powder.
• sulfur apparently acts so as to decrease the catalytic activity of nickel powder.
• the optimum content thereof is determined by the surface area of the nickel powder and is 30 to 500 ppm or less per specific surface area of 1 m 2 /g of the powder, in a weight proportion (calculated as sulfur atom) to the nickel powder of unit weight. If the content of sulfur is less than 30 ppm, the effect of adding sulfur is not demonstrated. If the content of sulfur is more than 500 ppm, sulfur remains in the multilayer component after firing and tends to degraded properties.
• the especially preferred range is 80 to 400 ppm.
• the amount of sulfur is measured, similarly to the amount of carbon, by a commercial carbon-sulfur analyzer or the like.
• the amount of hydroxyl groups bonded to the nickel powder surface be as low as possible.
• the resin will decompose even more vigorously at an early stage of firing at a comparatively low temperature.
• the amount of hydroxides on the nickel powder surface is high, dispersivity of the nickel powder in the organic vehicle tends to decrease.
• XPS X-ray photoelectron spectroscopy
• a wet reduction method a method of thermally decomposing a nickel compound, a chemical vapor deposition method (CVD) based on the reduction of a nickel compound in the gas phase, and a physical vapor deposition method (PVD) based on cooling a nickel vapor may be used as methods for manufacturing the nickel powder in accordance with the present invention.
• CVD chemical vapor deposition method
• PVD physical vapor deposition method
• a spray pyrolysis method described in Japanese Examined Patent Publication No. 63-31522B a method described in Japanese Patent Publications No.
• the nickel powder produced is heated in an oxidizing atmosphere, while preventing the aggregation of particles, thereby causing the prescribed level of surface oxidation. More specifically, the appropriate amount of oxidation can be attained without causing strong aggregation, by heating the nickel powder for about 1 to 10 hours in air at a temperature of 200°C or less.
• the above-described CVD method, PVD method, spray pyrolysis method, or a method of thermally decomposing a metal compound powder in a gas phase are preferred because a uniform oxidized layer can be formed on the nickel powder, without causing aggregation of the powder by mixing the powder with an oxidizing gas such as air, in a state where the nickel powder generated inside the reactor is effectively dispersed in the gas phase.
• the amount of surface oxidation of the produced powder can be regulated, for example, by the temperature at which the produced particles come into contact with the oxidizing gas.
• the surface oxidizing treatment may be conducted separately from or simultaneously with the below-described treatment for decreasing the carbon content or the treatment of adding sulfur. However, if the oxidation treatment is conducted prior to the carbon amount decrease treatment, the oxidized layer on the surface of nickel powder is reduced when carbon is removed, thereby causing aggregation of particles. Therefore, it is preferred that the oxidation treatment be conducted after the removal of carbon or simultaneously therewith.
• a nickel powder obtained, for example, by a wet reduction method or a method of reducing carbonyl nickel in a gas phase usually contain a comparatively large amount of carbon as an impurity.
• CVD method, PVD method, spray pyrolysis method, and method for thermal decomposition of a metal compound powder in a gas phase the residual quantity of carbon is comparatively low, but still the powder contains carbon in an amount larger that the range stipulated by the present invention. Furthermore, the amount of carbon varies depending on starting materials or equipment.
• a method for decreasing the content of carbon in the nickel powder to the range specified by the present invention can be employed by which the carbon component is burned and removed by heat treating the nickel powder in air at a temperature of 100 to 200°C or by decomposing and removing the carbon component with steam.
• a nickel carboxylate powder containing carbon is used as a starting material in a method of thermally decomposing a metal compound powder in a gas phase that is described in Japanese Patent Publication No. 2002-20809A
• the carbon component can be burned and removed by introducing steam or oxygen into a heating zone or cooling zone of a reaction vessel.
• the adequate amount of steam reacts with the carbon component, effectively decreasing the amount of carbon remaining in the powder produced, and the amount of carbon contained in the powder can be controlled by changing the amount of steam supplied. If an excess steam is supplied, the amount of hydroxyl groups present on the surface of the produced powder tends to increase.
• a method by which nickel powder is mixed with a sulfur powder and the mixture is heated in a sealed container or a method by which a gas containing sulfur such as hydrogen sulfide gas or sulfurous acid gas is caused to flow through and react with nickel powder can be used.
• a gas containing sulfur such as hydrogen sulfide gas or sulfurous acid gas
• a gas containing sulfur such as hydrogen sulfide gas or sulfurous acid gas
• the amount of sulfur in the powder can be controlled by varying the supplied amount of gas. Furthermore, with the spray pyrolysis method, a decomposable sulfur compound such as sulfuric acid, thiosulfuric acid or the like is dissolved in a starting material solution, thereby enabling the introduction of the predetermined amount of sulfur at the same time as the nickel powder is formed.
• the conductive paste in accordance with the present invention comprises the nickel powder as an electrically conductive powder and has this powder dispersed in a vehicle comprising a resin binder and a solvent.
• binders that have been usually used in conductive pastes can be used.
• examples of such binders including cellulose resins (e.g., ethyl cellulose, hydroxyethyl cellulose, etc.), acrylic resins, methacrylic resins, butyral resins, epoxy resins, phenolic resins, and rosin.
• cellulose resins e.g., ethyl cellulose, hydroxyethyl cellulose, etc.
• acrylic resins methacrylic resins
• butyral resins epoxy resins
• phenolic resins phenolic resins
• rosin No specific limitation is placed on the compounded amount of the resin binder. Usually, this amount is about 1 to 15 parts by weight per 100 parts by weight of the electrically conductive powder.
• the solvent No specific limitation is placed on the solvent, provided that it can dissolve the above-mentioned binder resin, and the solvents that have been usually used in pastes for inner electrodes can be appropriately selected and blended.
• organic solvents such as alcohols, ethers, esters, and hydrocarbons, water, or mixtures thereof can be used.
• the solvent is used in an amount of about 40 to 150 parts by weight per 100 parts by weight of the electrically conductive powder.
• the conductive paste in accordance with the present invention can contain other components that are usually used.
• inorganic powders such as ceramics having the composition identical or close to that of the ceramic contained in the ceramic sheet, glass, metal oxides such as alumina, silica, copper oxide, manganese oxide, and titanium oxide, and montmorillonite, organo-metallic compounds, plasticizers, dispersants, and surfactants can be appropriately compounded according to the object.
• the eclectically conductive paste in accordance with the present invention can be manufactured by the usual method by mixing and kneading the nickel powder and other additional components together with the binder resin and solvent, thereby uniformly dispersing the nickel powder.
• the conductive paste in accordance with the present invention is not limited to the paste form and may be in the form of a paint or ink.
• the eclectically conductive paste thus obtained can be used for forming inner electrodes of multilayer ceramic electronic components in particular, multilayer capacitors, multilayer inductors, multilayer actuators, and so on. Also, the conductive paste can be used for forming terminal electrodes of ceramic electronic components or thick conductor circuits.
• the multilayer ceramic electronic component is manufactured by the known method by using the conductive paste in accordance with the present invention for forming inner electrodes.
• a method for manufacturing a multilayer ceramic capacitor will be described below by way of an example.
• a dielectric ceramic starting material powder is dispersed in a resin binder, the dispersion is formed into sheets, by a doctor blade method or the like, and ceramic sheets are fabricated.
• a powder comprising as the main component a perovskite-type oxide of a barium titanate, strontium zirconate, and calcium strontium zirconate, or a compound obtained by replacing some of metal elements constituting such oxides with other metal elements can be used as the dielectric ceramic starting material powder. If necessary, a variety of additives for adjusting the capacitor characteristics can be mixed with those starting material powders.
• the conductive paste in accordance with the present invention is coated on the ceramic sheets obtained by using the usual method such as screen printing and dried to remove the solvent and form a dry film of the inner electrode paste of the predetermined pattern.
• the predetermined number of ceramic sheets having formed thereon the dry films of the inner electrode paste are stacked and laminated under pressure to fabricate an unfired multilayer body.
• the multilayer body is cut to the predetermined shape, treated to remove the binder at a temperature of about 250 to 350°C in an inert gas atmosphere or an inert gas atmosphere comprising a small amount of oxygen, thereby decomposing and dissipating the vehicle components.
• the multilayer body is then fired at a high temperature of about 1100 to 1350°C in a nonoxidizing atmosphere to sinter the dielectric layers and electrode layers, and a re-oxidizing treatment is further conducted, if necessary, to obtain a multilayer ceramic capacitor body.
• Terminal electrodes are thereafter formed by firing on both end surfaces of the multilayer ceramic capacitor body.
• the terminal electrodes may be also formed by applying a conductive paste onto both end surfaces of the chip obtained by cutting the unfired multilayer body and then co-firing with the multilayer body.
• a powder of nickel acetate tetrahydrate with a mean particle size of about 100 ⁇ m was supplied to a jet mill at a supply rate of 500 g/hr and pulverized and dispersed with a nitrogen gas at a flow rate of 200 L/min.
• the dispersion gas flow was introduced as is into a reaction tube located inside an electric furnace heated at a temperature of 1550°C, and the nickel acetate tetrahydrate was heated and decomposed to produce a nickel powder.
• the amount of carbon contained in the powder was decreased in this process by supplying steam from the vicinity of the port for introducing the dispersion gas flow into the reaction tube.
• the amount of carbon contained in the powder was controlled by the supplied amount of steam.
• a cooling pipe of the same diameter as the reaction tube was connected to the outlet port side of the reaction tube, a plurality of introducing pipes for introducing air were provided in the flow direction of gas in the cooling pipe, and the surface oxidation quantity of the produced powder was controlled by changing the temperature at which the produced particles come into contact with air according to the position in which the air was introduced.
• sulfur was introduced (sample numbers 11 to 14)
• hydrogen sulfide gas was separately supplied from the vicinity of the port for introducing the dispersion gas flow to the reaction tube, in the same manner as the steam.
• the amount of sulfur introduced in the powder was controlled by the supplied quantity of the hydrogen sulfide gas.
• the powder produced was recovered with a bag filter.
• sample numbers 1 to 15 were observed under a scanning electron microscope (SEM), and the formation of spherical particles was confirmed under all conditions. Furthermore, the formation of an oxidized layer on the surface of particles was also confirmed by observations under a scanning transmission electron microscope (STEM).
• SEM scanning electron microscope
• the specific surface area, mean particle size, oxygen content (ignition loss), carbon content, sulfur content, and proportion of surface hydroxyl groups were studied for each nickel powder. The results are shown in Table 1.
• the specific surface area was measured by a BET method.
• the mean particle size is a particle size calculated from the specific surface area.
• the ignition loss was represented as a weight variation percentage (%) by weighing about 2 g of the powder in an alumina boat, heating from room temperature to 900°C in a N 2 atmosphere containing 4% H 2 , cooling to room temperature, and measuring the variation of weight.
• the carbon content and sulfur content were measured with a carbon-sulfur analyzer (manufactured by Horiba Ltd., EMIA-320V).
• a Ni 2p spectrum of the powder surface was measured by XPS (KRATOS ANALYTICAL Co., Ltd., ESCA-3400), this spectrum was deconvoluted, and the proportion of the peak area attributed to a bonding of nickel and hydroxyl groups with respect to the total peak area in the Ni 2p spectrum was examined.
• a total of 100 part by weight of the nickel powders of sample numbers 1 to 15, 5 parts by weight of ethyl cellulose as a resin binder, and 95 parts by weight of dihydroterpineol were mixed and kneaded by using a three-roll mill to manufacture a conductive paste.
• the evaluation of binder removal characteristic of each of the conductive pastes thus obtained was conducted as follows.
• the conductive paste was applied onto a PET film to obtain a film thickness of 250 ⁇ m and dried at 150 °C to remove the solvent component.
• the dried film was heated to 500°C at a temperature rising rate of 20°C/min in a nitrogen gas atmosphere, and the decomposition initiation temperature of the resin was evaluated by conducting thermogravimetric measurements.
• Comparison of sample numbers 1 to 4 of Table 1 demonstrates that when the specific surface area and oxygen content are the same or almost the same, the higher is the carbon content, the lower is the decomposition initiation temperature of the resin in the conductive paste and the larger is the residual carbon amount after the heat treatment. Furthermore, comparison of sample number 1 and sample numbers 5 to 10 demonstrates that if the oxygen content is low, the decomposition initiation temperature drops and the residual carbon amount increases. Conversely, when the oxygen content is above a certain level, practically no changes occur with respect to the decomposition initiation temperature. Comparison of sample numbers 11 to 14 demonstrates that if sulfur is contained, the decomposition initiation temperature is risen and the residual carbon amount decreases. The results obtained for sample number 15, indicate that if the amount of surface hydroxyl groups is large, the decomposition initiation temperature tends to lower and the residual carbon amount tends to increase.
• the conductive pastes were then printed according in the predetermined pattern on barium titanate ceramic green sheets and dried to form dry films of conductive pastes serving as inner electrodes.
• the green sheets having the dry films of conductive pastes were stacked to obtain 30 dielectric effective layers, pressed together, and then cut to the predetermined dimensions to obtain unfired multilayer capacitor chips.
• the unfired chips were subjected to binder removal treatment for 12 hours at a temperature of 300°C in a nitrogen gas atmosphere and then fired for 2 hours at a peak temperature of 1250°C in a weakly reducing atmosphere comprising nitrogen gas containing hydrogen.
• Multilayer ceramic capacitor bodies were then fabricated by conducting re-oxidation treatment for 1 hour at a temperature of 1000°C in a weakly oxidizing atmosphere.
• the evaluation results relating to the continuity of electrodes demonstrate that the continuity tends to increase with the decrease in the residual carbon amount. Furthermore, even when the residual carbon amount is small, when the oxygen content is too high (sample number 10), the continuity of electrodes decreases, and when the ratio of surface hydroxyl groups is high (sample number 15), the continuity of electrodes tends to decrease.

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